Process for the manufacture of paper and paperboard
a technology applied in the field of paper and paperboard manufacture, can solve the problems of increased drainage rate, difficult to obtain the optimum balance of retention, and process can sometimes suffer the disadvantage, so as to improve formation and strength, increase the speed of the machine, and increase the drainage
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example 1
[0054]Confidential Trial in a Board Manufacturing Process
[0055]The mill produces folding box board on a five ply machine. The two outer plys are fourdrinier wires with 100% bleached chemical pulp and the 3 middle plys are Bell Bond formers with a 100% bleached groundwood furnish.
[0056]Machine speed depends on basis weight—lower basis weights (less than 250 gsm) usually run at higher machine speeds above 400 m / min and the higher basis weights run at lower speeds due to a steam (dryer) limitation. The retention aid in use is the Hydrocol system with the PAM added pre-screen and the bentonite added post screen. Bentonite is added with typical dosage rates of 0.9 kg / t into the outer plys and 1.2 to 1.5 kg / t into the middles plys. Cationic polyacrylamide (IV greater than 4 dl / g and charge density less than 3 mEq per gram) is added with a typical dosage rate 0.2 kg / t into the outer plys and 0.25 to 0.35 kg / t into the middles plys. These addition rates vary depending on furnish conditions ...
example 2
Confidential Trial in a Board Manufacturing Process at a Different Location from that of Example 1
[0057]The mill produces various grades of Kraft Liner on a two ply fourdrinier machine. The top ply furnish is always 100% unbleached kraft pulp and the base ply is a variable ratio of waste paper and unbleached kraft from 100% waste to a minimum 50% waste. Machine speed depends on basis weight—lower basis weights (less than 125 gsm) usually run at a maximum machine speed of 800 m / min and the higher basis weights run at lower speeds due to a steam (dryer) limitation. The retention aid in use is the Hydrocol system with the cationic polyacrylamide (IV greater than 4 dl / g and charge density less than 3 mEq per gram) added pre-screen and the bentonite added post screen. Bentonite is added with typical dosage rates of 1.4 to 2 kg / t into the top ply and 3.0 kg / t into the bottom ply. Cationic polyacrylamide is added with a typical dosage rate of 0.1 to 0.25 kg / t into the top ply and 0.25 to 0...
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